{"text_format":"1","workbook":"xlsx","n_sheets":3,"sheets":["CO2 FUNCTIONS","PUMP CYCLE","COMPRESSOR CYCLE"],"not_rendered":{"charts":4,"images":2,"macros":1,"external_links":0,"defined_names":2,"comments":0,"pivot_tables":0},"unopened":[],"bounds":{"document_bytes":16777216,"sheet_cells":100000,"rows_first":2000,"rows_last":500,"rows_between":2000,"halvings":0,"cell_chars":16384,"cell_head_chars":4096},"cells_cut":0,"cells_raw":0,"read":"whole","date_system":"1900"}

{"sheet":"CO2 FUNCTIONS","index":0,"n_rows":104,"n_cols":7,"rows_kept":104,"cut":false,"hidden":false,"merged":[]}
[null,"Physical Properties for Carbon Dioxide"]
[null,"Tohoku University, Version 3.4 (CO2v34.bas)",null,null,null,"For Educational Use Only!"]
[null,"Report errors to R. L. Smith;  Email: smith@scf.che.tohoku.ac.jp"]
["Hint:  Select green box to see how to use function.  Be careful for units!  First letter of function is dependent variable;  other letters are independent variables; 1=CO2."]
["Example:  VPT1(P,T) is Specific Volume as a function of Pressure and Temperature."]
["       Function units are in kg, m3, C, Pa, J"]
["Fundamental Constants","Function Name","Examples"]
["  Tc: critical temperature of CO2 (in C)","CO2TC()",{"$f":"CO2TC()","v":{"$error":"#NAME?"}},"oC"]
["  Pc: critical pressure of CO2    (in Pa)","CO2PC()",{"$f":"CO2PC()/1000000","v":{"$error":"#NAME?"}},"MPa"]
["  Vc: critical volume of CO2      (m3/kg)","CO2VC()",{"$f":"CO2VC()","v":{"$error":"#NAME?"}},"m3/kg"]
["  rc: critical density of CO2     (kg/m3)","CO2rhoc()",{"$f":"CO2rhoc()","v":{"$error":"#NAME?"}},"kg/m3"]
["  Mw: molecular weight of CO2     (kg/mol)","CO2MW()",{"$f":"co2mw()","v":{"$error":"#NAME?"}},"kg/mol"]
[]
["Solid",null,null,"T [oC]","P [Pa]","Calculated Value"]
["  Pm:  melting pressure (S-L)","PMELT1(T)",null,-55.6,null,{"$f":"PMELT1(D15)/1000000","v":{"$error":"#NAME?"}},"MPa"]
["  Tm:  melting temperature (S-L)","TMELT1(P)",null,null,5000000,{"$f":"TMELT1(E16)","v":{"$error":"#NAME?"}},"oC"]
["  Psub:  sublimation pressure (S-V)","PSUB1(T)",null,-85,null,{"$f":"PSUB1(D17)/1000000","v":{"$error":"#NAME?"}},"MPa"]
[]
["Pressure-Volume (density)-Temperature"]
["Based on: R. Span and W. Wagner, A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple-Point Temperature to 1100 K at Pressures up to 800 MPa, J. Phys. Chem. Ref. Data 25(6), 1509-1596 (1996)."]
[null,null,"r [kg/m3]","T [oC]","P [Pa]","Calculated Value"]
["Saturation Curve: Vapor-liquid Equilibrium"]
["  Psat:  Vapor pressure (saturation pressure), Pa","PSAT1(T)",null,25,null,{"$f":"PSAT1(D23)/1000000","v":{"$error":"#NAME?"}},"MPa"]
["  Tsat:  Vapor temperature (saturation temperature), oC","TSAT1(P)",null,null,7000000,{"$f":"TSAT1(E24)","v":{"$error":"#NAME?"}},"oC"]
["  Svap:  Heat (enthalpy) of vaporization, J/kg","HVAPT1(T)",null,25,null,{"$f":"HVAPT1(D25)*co2mw()/1000","v":{"$error":"#NAME?"}},"kJ/mol"]
["  Hvap:  Entropy of vaporization, J/kg K","SVAPT1(T)",null,25,null,{"$f":"SVAPT1(D26)","v":{"$error":"#NAME?"}},"J/kg K"]
["     Liquid phase (saturated)"]
["r: Density, kg/m3","RHOLT1(T)",null,25,null,{"$f":"rholt1(D28)","v":{"$error":"#NAME?"}},"kg/m3"]
["H: Enthalpy, H, J/kg","HLT1(T)",null,25,null,{"$f":"_HLT1(D29)","v":{"$error":"#NAME?"}},"J/kg"]
["S: Entropy, S, J/kg K","SLT1(T)",null,25,null,{"$f":"_SLT1(D30)","v":{"$error":"#NAME?"}},"J/kg K"]
["Cp: constant pressure heat capacity, J/kg K","CPLT1(T)",null,25,null,{"$f":"CPLT1(D31)","v":{"$error":"#NAME?"}},"J/kg K"]
["Cv: constant volume heat capacity, J/kg K","CVLT1(T)",null,25,null,{"$f":"CVLT1(D32)","v":{"$error":"#NAME?"}},"J/kg K"]
["     Gas/vapor phase (saturated)"]
["r: Density, kg/m3","RHOGT1(T)",null,25,null,{"$f":"rhogt1(D34)","v":{"$error":"#NAME?"}},"kg/m3"]
["H: Enthalpy, H, J/kg","HGT1(T)",null,25,null,{"$f":"_HGT1(D35)","v":{"$error":"#NAME?"}},"J/kg"]
["S: Entropy, S, J/kg K","SGT1(T)",null,25,null,{"$f":"_SGT1(D36)","v":{"$error":"#NAME?"}},"J/kg K"]
["Cp: constant pressure heat capacity, J/kg K","CPGT1(T)",null,25,null,{"$f":"CPGT1(D37)","v":{"$error":"#NAME?"}},"J/kg K"]
["Cv: constant volume heat capacity, J/kg K","CVGT1(T)",null,25,null,{"$f":"CVGT1(D38)","v":{"$error":"#NAME?"}},"J/kg K"]
["Single Phase Region"]
["Note: U, H, S, Cp, Cv can be used"]
["on the saturation boundary"]
["  T,P functions",null,"r [kg/m3]","T [oC]","P [Pa]","Calculated Value"]
["    V: specific volume, Wagner eqn., m3/kg","VTP1(T,P)",null,40,10000000,{"$f":"_VTP1(D43,E43)","v":{"$error":"#NAME?"}},"m3/kg"]
["    r: Density, kg/m3","RHOTP1(T,P)",null,40,10000000,{"$f":"rhotp1(D44,E44)","v":{"$error":"#NAME?"}},"kg/m3"]
["    f: fugacity, Pa","FUGTP1(T,P)",null,40,10000000,{"$f":"fugtp1(D45,E45)/1000000","v":{"$error":"#NAME?"}},"MPa"]
["    U: internal energy","UTP1(T,P)",null,40,10000000,{"$f":"_UTP1(D46,E46)","v":{"$error":"#NAME?"}},"J/kg"]
["    H: Enthalpy, H, J/kg","HTP1(T,P)",null,40,10000000,{"$f":"_HTP1(D47,E47)","v":{"$error":"#NAME?"}},"J/kg"]
["    S: Entropy, S, J/kg K","STP1(T,P)",null,40,10000000,{"$f":"_STP1(D48,E48)","v":{"$error":"#NAME?"}},"J/kg K"]
["    Cv: constant volume heat capacity, J/kg K","CVTP1(T,P)",null,40,10000000,{"$f":"CVTP1(D49,E49)","v":{"$error":"#NAME?"}},"J/kg K"]
["    Cp: constant pressure heat capacity, J/kg K","CPTP1(T,P)",null,40,10000000,{"$f":"cptp1(D50,E50)","v":{"$error":"#NAME?"}},"J/kg K"]
["    w: speed of sound, m/s","WTP1(T,P)",null,40,10000000,{"$f":"_WTP1(D51,E51)","v":{"$error":"#NAME?"}},"m/s"]
["  r,T functions"]
["     P: pressure, Wagner eqn., Pa","PRT1(RHO,T)",628.61,40,null,{"$f":"_PRT1(C53,D53)/1000000","v":{"$error":"#NAME?"}},"MPa"]
["     f: fugacity, Pa","FUGRT1(T,RHO)",628.61,40,null,{"$f":"FUGRT1(C54,D54)/1000000","v":{"$error":"#NAME?"}},"MPa"]
["    U:  internal energy","URT1(RHO,T)",628.61,40,null,{"$f":"_URT1(C55,D55)","v":{"$error":"#NAME?"}},"J/kg"]
["    H: Enthalpy, H, J/kg","HRT1(RHO,T)",628.61,40,null,{"$f":"_HRT1(C56,D56)","v":{"$error":"#NAME?"}},"J/kg"]
["    S: Entropy, S, J/kg K","SRT1(RHO,T)",628.61,40,null,{"$f":"_SRT1(C57,D57)","v":{"$error":"#NAME?"}},"J/kg K"]
["    Cv: constant volume heat capacity, J/kg K","CVRT1(RHO,T)",628.61,40,null,{"$f":"CVRT1(C58,D58)","v":{"$error":"#NAME?"}},"J/kg K"]
["    Cp: constant pressure heat capacity, J/kg K","CPRT1(RHO,T)",628.61,40,null,{"$f":"CPRT1(C59,D59)","v":{"$error":"#NAME?"}},"J/kg K"]
["    w: speed of sound, m/s","WRT1(RHOH,T)",628.61,40,null,{"$f":"_WRT1(C60,D60)","v":{"$error":"#NAME?"}},"m/s"]
["  Virial Coefficients"]
["     B: Second virial coefficient B, m3/kg","VIRIALBT1(T)",null,25,null,{"$f":"VIRIALBT1(D62)","v":{"$error":"#NAME?"}},"m3/kg"]
["     C: Third virial coefficient C, m6/kg2","VIRIALCT1(T)",null,25,null,{"$f":"VIRIALCT1(D63)","v":{"$error":"#NAME?"}},"m6/kg2"]
["Functions Useful for Compressors/Pumps/\nExpansions through Valves",null,"S J/kg K",null,"H J/kg"]
["  T:  single phase temperature at P, S","TPS1(P,S)",-1382.7457662131249,10000000,null,{"$f":"_TPS1(D65,C65)","v":{"$error":"#NAME?"}},"oC"]
["  T:  single phase temperature at P, H","TPH1(P,H)",null,10000000,-193737.32837687424,{"$f":"_TPH1(D66,E66)","v":{"$error":"#NAME?"}},"oC"]
[]
[]
[null,null,"r [kg/m3]","T [oC]","P [Pa]","Calculated Value"]
["  Joule-Thomson coefficient mu = (dT/dP)h","JTRT1(RHO,T)",628.61,40,null,{"$f":"JTRT1(C70,D70)*1000000","v":{"$error":"#NAME?"}},"K/MPa"]
["  Isothermal throttling coefficient delt = (dh/dP)T","DELTRT1(RHO,T)",628.61,40,null,{"$f":"DELTRT1(C71,D71)","v":{"$error":"#NAME?"}},"J/kg Pa"]
["  Isentropic temperature pressure coefficient bs = (dT/dP)s","BETASRT1(RHO,T)",628.61,40,null,{"$f":"BETASRT1(C72,D72)*1000000","v":{"$error":"#NAME?"}},"K/MPa"]
["Derivative Properties"]
["  T,P functions",null,"r [kg/m3]","T [oC]","P [Pa]","Calculated Value"]
["     dP/dT derivative","DPDTTP1(T, P)",null,40,10000000,{"$f":"DPDTTP1(D75, E75)/1000000","v":{"$error":"#NAME?"}},"MPa/K"]
["     dP/drho derivative = (dP/drho)T","DPDRTP1(T,P)",null,40,10000000,{"$f":"DPDRTP1(D76,E76)/1000000","v":{"$error":"#NAME?"}},"MPa/(kg/m3)"]
["     drho/dT derivative = (drho/dT)P","DRDTTP1(T,P)",null,40,10000000,{"$f":"DRDTTP1(D77,E77)","v":{"$error":"#NAME?"}},"(kg/m3 K)"]
["     Isothermal compressibility = (1/rho)*(drho/dP)T","BETATTP1(T,P)",null,40,10000000,{"$f":"BETATTP1(D78,E78)*1000000","v":{"$error":"#NAME?"}},"1/MPa"]
["     Volume coefficient of expansion =  (1/V)*(dV/dT)P","BETAPTP1(T,P)",null,40,10000000,{"$f":"BETAPTP1(D79,E79)","v":{"$error":"#NAME?"}},"1/K"]
["  r,T functions"]
["     dP/dT derivative","DPDTRT1(RHO,T)",628.61,40,null,{"$f":"DPDTRT1(C81,D81)/1000000","v":{"$error":"#NAME?"}},"MPa/K"]
["     dP/drho derivative = (dP/drho)T","DPDRRT1(RHO,T)",628.61,40,null,{"$f":"DPDRRT1(C82,D82)/1000000","v":{"$error":"#NAME?"}},"MPa/(kg/m3)"]
["     drho/dT derivative = (drho/dT)P (derived)","DRDTRT1(RHO,T)",628.61,40,null,{"$f":"DRDTRT1(C83,D83)","v":{"$error":"#NAME?"}},"(kg/m3 K)"]
["     Isothermal compressibility = -(1/V)*(dV/dP)T","BETATRT1(RHO,T)",628.61,40,null,{"$f":"BETATRT1(C84,D84)*1000000","v":{"$error":"#NAME?"}},"1/MPa"]
["     Volume coefficient of expansion =  -(1/V)*(dV/dT)P","BETAPRT1(RHO,T)",628.61,40,null,{"$f":"BETAPRT1(C85,D85)","v":{"$error":"#NAME?"}},"1/K"]
["Transport Properties"]
["Based on correlations in Reid, Prausnitz and Poling (1987)"]
["     Liquid phase (saturated)",null,null,"T [oC]",null,"Calculated Value"]
["               Viscosity, Pa s","VMULT1(T)",null,25,null,{"$f":"vmult1(D89)","v":{"$error":"#NAME?"}},"Pa s"]
["               Kinematic viscosity (dense gas),  (=mu/rho),  m2/s  ","VNULT1(T)",null,25,null,{"$f":"vnult1(D90)","v":{"$error":"#NAME?"}},"m2/s"]
["               Surface tension, N/m","SIGMAT1(T)",null,25,null,{"$f":"SIGMAT1(D91)","v":{"$error":"#NAME?"}},"N/m"]
["     Gas/vapor phase (saturated)"]
["               Viscosity, Pa s","VMUGT1(T)",null,25,null,{"$f":"vmugt1(D93)","v":{"$error":"#NAME?"}},"Pa s"]
["               Kinematic viscosity (dense gas),  (=mu/rho),  m2/s  ","VNUGT1(T)",null,25,null,{"$f":"vnugt1(D94)","v":{"$error":"#NAME?"}},"m2/s"]
["               Ideal gas thermal conductivity, W/(m K)","KIDT1(T)",null,25,null,{"$f":"KIDT1(D95)","v":{"$error":"#NAME?"}},"W/(m K)"]
["     Single Phase (Gas/vapor) Region"]
["          T,P functions",null,"r [kg/m3]","T [oC]","P [Pa]","Calculated Value"]
["               Viscosity (dense gas), Pa s","VMUTP1(T,P)",null,40,10000000,{"$f":"VMUTP1(D98,E98)","v":{"$error":"#NAME?"}},"Pa s"]
["               Kinematic viscosity (dense gas),  (=mu/rho),  m2/s  ","VNUTP1(T,P)",null,40,10000000,{"$f":"vnutp1(D99,E99)","v":{"$error":"#NAME?"}},"m3/s"]
["               Thermal conductivity (dense gas), W/(m K)","kTP1(T,P)",null,40,10000000,{"$f":"_kTP1(D100,E100)","v":{"$error":"#NAME?"}},"W/(m K)"]
["         r,T functions"]
["               Viscosity (dense gas), Pa s","VMURT1(RHO,T)",628.61,40,null,{"$f":"vmurt1(C102,D102)","v":{"$error":"#NAME?"}},"Pa s"]
["               Kinematic viscosity (dense gas),  (=mu/rho),  m2/s  ","VNURT1(RHO,T)",628.61,40,null,{"$f":"VNURT1(C103,D103)","v":{"$error":"#NAME?"}},"m2/s"]
["               Thermal conductivity (dense gas), W/(m K)","kRT1(RHO,T)",628.61,40,null,{"$f":"_kRT1(C104,D104)","v":{"$error":"#NAME?"}},"W/(m K)"]

{"sheet":"PUMP CYCLE","index":1,"n_rows":59,"n_cols":31,"rows_kept":59,"cut":false,"hidden":false,"merged":[]}
[null,null,null,"PUMP (Liquid - Vapor Cycle)",null,null,null,null,"SCF Extraction Cycle Energy Requirements: Pump (liquid CO2 feed)"]
[null,null,null,null,null,null,null,null,null,"based the Wagner Equation of State-version 7.0",null,null,null,"Report errors to R.L.Smith. Email: smith@scf.che.tohoku.ac.jp"]
[null,null,null,null,null,null,null,null,null,"Version 1.6"]
[]
["R. Span and W. Wagner, A New Equation of State for Carbon Dioxide Covering ",null,null,null,null,null,"Point","T [C]","P [MPa]","H [kJ/kg]","X","S [kJ/kg K]","rho [kg/m3]","Comments","HL [kJ/kg]","HG [kJ/kg]","rhoL [kg/m3]","rhoG [kg/m3]","S [kJ/kg K]","S [kJ/kg K]"]
["the Fluid Regionfrom the Triple-Point Temperature to 1100 K at Pressures up to 800 MPa,",null,null,null,null,null,2,{"$f":"T_PS1(I6*1000000,L6*1000)","v":14.7933221371493},{"$f":"I8","v":15},{"$f":"H_TP1(H6,I6*1000000)/1000","v":225.31647881236037},0,{"$f":"L11","v":1.0460701896854798},{"$f":"rho_tp1(H6,I6*1000000)","v":930.80792111958772},"Compressed liquid",{"$f":"IF(H6<CO2_TC(),HL_t1(H6)/1000,H_TP1(H6,I6*1000000)/1000)","v":239.3734578780242},{"$f":"IF(H6<CO2_TC(),HG_T1(H6)/1000,H_TP1(H6,I6*1000000)/1000)","v":416.93017456483864},{"$f":"IF(H6<CO2_TC(),rhol_t1(H6),rho_tp1(H6,I6*1000000))","v":822.9650407093693},{"$f":"IF(H6<CO2_TC(),rhog_T1(H6),rho_tp1(H6,I6*1000000))","v":159.54823687119594},{"$f":"IF(H6<CO2_TC(),sl_t1(H6)/1000,s_tp1(H6,I6*1000000)/1000)","v":1.1338362191820608},{"$f":"IF(H6<CO2_TC(),sG_T1(H6)/1000,s_tp1(H6,I6*1000000)/1000)","v":1.7504687108228603}]
["J. Phys. Chem. Ref. Data 25(6), 1509-1596 (1996).",null,null,null,null,null,3,40,15,{"$f":"H_TP1(H7,I7*1000000)/1000","v":285.47880137140351},{"$f":"IF(AND(J7>O7,J7<P7),(J7-O7)/(P7-O7),1)","v":1},{"$f":"s_tp1(H7,I7*1000000)/1000","v":1.2460796017586968},{"$f":"rho_tp1(H7,I7*1000000)","v":780.232878564732},"Supercritical fluid state-extraction",{"$f":"IF(H7<CO2_TC(),HL_t1(H7)/1000,H_TP1(H7,I7*1000000)/1000)","v":285.47880137140351},{"$f":"IF(H7<CO2_TC(),HG_T1(H7)/1000,H_TP1(H7,I7*1000000)/1000)","v":285.47880137140351},{"$f":"IF(H7<CO2_TC(),rhol_t1(H7),rho_tp1(H7,I7*1000000))","v":780.232878564732},{"$f":"IF(H7<CO2_TC(),rhog_T1(H7),rho_tp1(H7,I7*1000000))","v":780.232878564732},{"$f":"IF(H7<CO2_TC(),sl_t1(H7)/1000,s_tp1(H7,I7*1000000)/1000)","v":1.2460796017586968},{"$f":"IF(H7<CO2_TC(),sG_T1(H7)/1000,s_tp1(H7,I7*1000000)/1000)","v":1.2460796017586968}]
[null,null,null,null,null,null,4,{"$f":"H7","v":40},{"$f":"I7","v":15},{"$f":"H_TP1(H8,I8*1000000)/1000","v":285.47880137140351},{"$f":"IF(AND(J8>O8,J8<P8),(J8-O8)/(P8-O8),1)","v":1},{"$f":"s_tp1(H8,I8*1000000)/1000","v":1.2460796017586968},{"$f":"rho_tp1(H8,I8*1000000)","v":780.232878564732},"SC fluid state saturated with solute",{"$f":"IF(H8<CO2_TC(),HL_t1(H8)/1000,H_TP1(H8,I8*1000000)/1000)","v":285.47880137140351},{"$f":"IF(H8<CO2_TC(),HG_T1(H8)/1000,H_TP1(H8,I8*1000000)/1000)","v":285.47880137140351},{"$f":"IF(H8<CO2_TC(),rhol_t1(H8),rho_tp1(H8,I8*1000000))","v":780.232878564732},{"$f":"IF(H8<CO2_TC(),rhog_T1(H8),rho_tp1(H8,I8*1000000))","v":780.232878564732},{"$f":"IF(H8<CO2_TC(),sl_t1(H8)/1000,s_tp1(H8,I8*1000000)/1000)","v":1.2460796017586968},{"$f":"IF(H8<CO2_TC(),sG_T1(H8)/1000,s_tp1(H8,I8*1000000)/1000)","v":1.2460796017586968}]
[null,null,null,null,null,null,5,{"$f":"T_PH1(I9*1000000,J9*1000)","v":5.3001936869808679},4,{"$f":"J8","v":285.47880137140351},{"$f":"IF(AND(J9>O9,J9<P9),(J9-O9)/(P9-O9),1)","v":0.33745651206222227},{"$f":"IF(K9<1,K9*T9+(1-K9)*S9,s_tp1(H9,I9*1000000)/1000)","v":1.3053804781877099},{"$f":"IF(K9<1,K9*R9+(1-K9)*Q9,rho_tp1(H9,I9*1000000))","v":631.38497837567809},"System state decided by final enthalpy",{"$f":"IF(H9<CO2_TC(),HL_t1(H9)/1000,H_TP1(H9,I9*1000000)/1000)","v":213.27290653224702},{"$f":"IF(H9<CO2_TC(),HG_T1(H9)/1000,H_TP1(H9,I9*1000000)/1000)","v":427.24386948063051},{"$f":"IF(H9<CO2_TC(),rhol_t1(H9),rho_tp1(H9,I9*1000000))","v":894.02107092837412},{"$f":"IF(H9<CO2_TC(),rhog_T1(H9),rho_tp1(H9,I9*1000000))","v":115.73977196126576},{"$f":"IF(H9<CO2_TC(),sl_t1(H9)/1000,s_tp1(H9,I9*1000000)/1000)","v":1.0460689241767194},{"$f":"IF(H9<CO2_TC(),sG_T1(H9)/1000,s_tp1(H9,I9*1000000)/1000)","v":1.8144984691462864}]
[null,null,null,null,null,null,6,{"$f":"H9","v":5.3001936869808679},{"$f":"I9","v":4},{"$f":"IF(K9=1,J9,P9)","v":427.24386948063051},{"$f":"IF(AND(J10>O10,J10<P10),(J10-O10)/(P10-O10),1)","v":1},{"$f":"sG_T1(H10)/1000","v":1.8144984691462864},{"$f":"rho_tp1(H10,I10*1000000)","v":115.73977196010858},"Saturated vapor",{"$f":"IF(H10<CO2_TC(),HL_t1(H10)/1000,H_TP1(H10,I10*1000000)/1000)","v":213.27290653224702},{"$f":"IF(H10<CO2_TC(),HG_T1(H10)/1000,H_TP1(H10,I10*1000000)/1000)","v":427.24386948063051},{"$f":"IF(H10<CO2_TC(),rhol_t1(H10),rho_tp1(H10,I10*1000000))","v":894.02107092837412},{"$f":"IF(H10<CO2_TC(),rhog_T1(H10),rho_tp1(H10,I10*1000000))","v":115.73977196126576},{"$f":"IF(H10<CO2_TC(),sl_t1(H10)/1000,s_tp1(H10,I10*1000000)/1000)","v":1.0460689241767194},{"$f":"IF(H10<CO2_TC(),sG_T1(H10)/1000,s_tp1(H10,I10*1000000)/1000)","v":1.8144984691462864}]
[null,null,null,null,null,null,1,{"$f":"Tsat_P1(I11*1000000)","v":5.3003369391846737},{"$f":"I10","v":4},{"$f":"HL_t1(H11)/1000","v":213.27327530153636},0,{"$f":"sl_t1(H11)/1000","v":1.0460701896854798},{"$f":"rhol_t1(H11)","v":894.02012026312593},"Saturated liquid",{"$f":"IF(H11<CO2_TC(),HL_t1(H11)/1000,H_TP1(H11,I11*1000000)/1000)","v":213.27327530153636},{"$f":"IF(H11<CO2_TC(),HG_T1(H11)/1000,H_TP1(H11,I11*1000000)/1000)","v":427.24375428590838},{"$f":"IF(H11<CO2_TC(),rhol_t1(H11),rho_tp1(H11,I11*1000000))","v":894.02012026312593},{"$f":"IF(H11<CO2_TC(),rhog_T1(H11),rho_tp1(H11,I11*1000000))","v":115.74031024306707},{"$f":"IF(H11<CO2_TC(),sl_t1(H11)/1000,s_tp1(H11,I11*1000000)/1000)","v":1.0460701896854798},{"$f":"IF(H11<CO2_TC(),sG_T1(H11)/1000,s_tp1(H11,I11*1000000)/1000)","v":1.8144976012711944}]
[]
[]
[null,null,null,null,null,null,null,null,null,"Solvent Flow Rate",null,0.3,"kg/s"]
[]
[]
[null,null,null,null,null,null,null,null,null,"Heating and Cooling Requirements"]
[null,null,null,null,null,null,null,null,null,"Q32",{"$f":"(J7-J6)*L14","v":18.04869676771294},"kW"]
[null,null,null,null,null,null,null,null,null,"Q65",{"$f":"(J10-J9)*L14","v":42.529520432768102},"kW",null,null,null,null,null,null,null,"Tables for the Point-to-Point curves in the above plots.  "]
[null,null,null,null,null,null,null,null,null,"Q16",{"$f":"(J11-J10)*L14","v":-64.191178253728239},"kW"]
[]
[null,null,null,null,null,null,null,null,null,"Electrical Energy Requirements"]
[null,null,null,null,null,null,null,null,null,"W21",{"$f":"(J6-J11)*L14","v":3.6129610532472043},"kW"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"P [MPa]","T [C]","rho [kg/m3]","S [kJ/kg K]","H [kJ/kg]"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Path 1-2",{"$f":"$I$11","v":4},{"$f":"T_PS1(T25*1000000,W25*1000)","v":5.3001936865433894},{"$f":"rho_tp1(U25,T25*1000000)","v":894.04245075760969},{"$f":"$L$11","v":1.0460701896854798}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"T25+($I$6-$I$11)/10","v":5.0999999999999996},6.3820038054711832,898.51571814345675,{"$f":"$L$11","v":1.0460701896854798}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"T26+($I$6-$I$11)/10","v":6.1999999999999993},7.4237629965111394,902.73433747531749,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,7.2999999999999989,8.4322946301926347,906.73869861259425,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,8.3999999999999986,9.4112315236011188,910.56436152030551,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,9.4999999999999982,10.363423378460292,914.23607200809261,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10.599999999999998,11.291198060205051,917.77215602942215,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,11.699999999999998,12.196509612800078,921.18685056645495,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,12.799999999999997,13.081029917509193,924.491624367746,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,13.899999999999997,13.946209790425389,927.69597246355306,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,14.999999999999996,14.793322137149318,930.80792111958772,1.0460701896854798]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Path 2-3",{"$f":"$I$6","v":15},{"$f":"$H$6","v":14.7933221371493},930.80792111958772,{"$f":"s_tp1(U36,T36*1000000)/1000","v":1.0460701896853939}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"$I$6","v":15},{"$f":"U36+($H$7-$H$6)/10","v":17.31398992343437},918.01397501178542,{"$f":"s_tp1(U37,T37*1000000)/1000","v":1.0652114395265446}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,{"$f":"U37+($H$7-$H$6)/10","v":19.834657709719441},904.8351245071924,{"$f":"s_tp1(U38,T38*1000000)/1000","v":1.084456589441803}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,22.355325496004511,891.23634630729975,{"$f":"s_tp1(U39,T39*1000000)/1000","v":1.1038323233195737}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,24.875993282289581,877.17721909233819,{"$f":"s_tp1(U40,T40*1000000)/1000","v":1.123369379181435}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,27.396661068574652,862.6115380916533,{"$f":"s_tp1(U41,T41*1000000)/1000","v":1.1431022968464695}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,29.917328854859722,847.48756620989502,{"$f":"s_tp1(U42,T42*1000000)/1000","v":1.163068574853136}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,32.437996641144792,831.74894237272963,{"$f":"s_tp1(U43,T43*1000000)/1000","v":1.1833075900810079}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,34.958664427429859,815.33585998394051,{"$f":"s_tp1(U44,T44*1000000)/1000","v":1.2038599987321157}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,37.479332213714926,798.18575524576818,{"$f":"s_tp1(U45,T45*1000000)/1000","v":1.2247684149347668}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,39.999999999999993,780.232878564732,{"$f":"s_tp1(U46,T46*1000000)/1000","v":1.2460796017586968},null,"X","HL","HG","SL","SG","RHOL","RHOG"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Path 3-4-5",{"$f":"$I$7","v":15},{"$f":"IF(AND(Y47>0,Y47<1),Tsat_P1(T47*1000000),T_PH1(T47*1000000,X47*1000))","v":39.99999999999995},{"$f":"IF(Y47=1,rho_tp1(U47,T47*1000000),Y47*AE47+(1-Y47)*AD47)","v":780.23287856473189},{"$f":"IF(Y47=1,s_tp1(U47,T47*1000000)/1000,Y47*AC47+(1-Y47)*AB47)","v":1.246079601758697},{"$f":"$J$7","v":285.47880137140351},{"$f":"IF(AND(X47>Z47,X47<AA47),(X47-Z47)/(AA47-Z47),1)","v":1},{"$f":"IF(T47*1000000<CO2_PC(),HL_t1(Tsat_P1(T47*1000000))/1000,0)","v":0},{"$f":"IF(T47*1000000<CO2_PC(),HG_T1(Tsat_P1(T47*1000000))/1000,0)","v":0},{"$f":"IF(U47<CO2_TC(),sl_t1(U47)/1000,s_tp1(U47,T47*1000000)/1000)","v":1.246079601758697},{"$f":"IF(U47<CO2_TC(),sG_T1(U47)/1000,s_tp1(U47,T47*1000000)/1000)","v":1.246079601758697},{"$f":"IF(U47<CO2_TC(),rhol_t1(U47),rho_tp1(U47,T47*1000000))","v":780.23287856473189},{"$f":"IF(U47<CO2_TC(),rhog_T1(U47),rho_tp1(U47,T47*1000000))","v":780.23287856473189}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"T47+($I$9-$I$7)/10","v":13.9},38.929350936943528,770.03239115107851,{"$f":"IF(Y48=1,s_tp1(U48,T48*1000000)/1000,Y48*AC48+(1-Y48)*AB48)","v":1.2506187071218493},{"$f":"$J$7","v":285.47880137140351},{"$f":"IF(AND(X48>Z48,X48<AA48),(X48-Z48)/(AA48-Z48),1)","v":1},{"$f":"IF(T48*1000000<CO2_PC(),HL_t1(Tsat_P1(T48*1000000))/1000,0)","v":0},{"$f":"IF(T48*1000000<CO2_PC(),HG_T1(Tsat_P1(T48*1000000))/1000,0)","v":0},{"$f":"IF(U48<CO2_TC(),sl_t1(U48)/1000,s_tp1(U48,T48*1000000)/1000)","v":1.2506187071218493},{"$f":"IF(U48<CO2_TC(),sG_T1(U48)/1000,s_tp1(U48,T48*1000000)/1000)","v":1.2506187071218493},{"$f":"IF(U48<CO2_TC(),rhol_t1(U48),rho_tp1(U48,T48*1000000))","v":770.03239115107851},{"$f":"IF(U48<CO2_TC(),rhog_T1(U48),rho_tp1(U48,T48*1000000))","v":770.03239115107851}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"T48+($I$9-$I$7)/10","v":12.8},37.7355126645637,759.07699901187243,{"$f":"IF(Y49=1,s_tp1(U49,T49*1000000)/1000,Y49*AC49+(1-Y49)*AB49)","v":1.2552372601422923},285.47880137140351,1,{"$f":"IF(T49*1000000<CO2_PC(),HL_t1(Tsat_P1(T49*1000000))/1000,0)","v":0},{"$f":"IF(T49*1000000<CO2_PC(),HG_T1(Tsat_P1(T49*1000000))/1000,0)","v":0},{"$f":"IF(U49<CO2_TC(),sl_t1(U49)/1000,s_tp1(U49,T49*1000000)/1000)","v":1.2552372601422923},{"$f":"IF(U49<CO2_TC(),sG_T1(U49)/1000,s_tp1(U49,T49*1000000)/1000)","v":1.2552372601422923},{"$f":"IF(U49<CO2_TC(),rhol_t1(U49),rho_tp1(U49,T49*1000000))","v":759.07699901187243},{"$f":"IF(U49<CO2_TC(),rhog_T1(U49),rho_tp1(U49,T49*1000000))","v":759.07699901187243}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,11.700000000000001,36.395634300051562,747.20581508407827,{"$f":"IF(Y50=1,s_tp1(U50,T50*1000000)/1000,Y50*AC50+(1-Y50)*AB50)","v":1.2599448354280192},285.47880137140351,1,{"$f":"IF(T50*1000000<CO2_PC(),HL_t1(Tsat_P1(T50*1000000))/1000,0)","v":0},{"$f":"IF(T50*1000000<CO2_PC(),HG_T1(Tsat_P1(T50*1000000))/1000,0)","v":0},{"$f":"IF(U50<CO2_TC(),sl_t1(U50)/1000,s_tp1(U50,T50*1000000)/1000)","v":1.2599448354280192},{"$f":"IF(U50<CO2_TC(),sG_T1(U50)/1000,s_tp1(U50,T50*1000000)/1000)","v":1.2599448354280192},{"$f":"IF(U50<CO2_TC(),rhol_t1(U50),rho_tp1(U50,T50*1000000))","v":747.20581508407827},{"$f":"IF(U50<CO2_TC(),rhog_T1(U50),rho_tp1(U50,T50*1000000))","v":747.20581508407827}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10.600000000000001,34.878677392225036,734.18540496133448,{"$f":"IF(Y51=1,s_tp1(U51,T51*1000000)/1000,Y51*AC51+(1-Y51)*AB51)","v":1.2647534762416042},285.47880137140351,1,{"$f":"IF(T51*1000000<CO2_PC(),HL_t1(Tsat_P1(T51*1000000))/1000,0)","v":0},{"$f":"IF(T51*1000000<CO2_PC(),HG_T1(Tsat_P1(T51*1000000))/1000,0)","v":0},{"$f":"IF(U51<CO2_TC(),sl_t1(U51)/1000,s_tp1(U51,T51*1000000)/1000)","v":1.2647534762416042},{"$f":"IF(U51<CO2_TC(),sG_T1(U51)/1000,s_tp1(U51,T51*1000000)/1000)","v":1.2647534762416042},{"$f":"IF(U51<CO2_TC(),rhol_t1(U51),rho_tp1(U51,T51*1000000))","v":734.18540496133448},{"$f":"IF(U51<CO2_TC(),rhog_T1(U51),rho_tp1(U51,T51*1000000))","v":734.18540496133448}]
[null,null,null,null,null,null,null,null,null,null,"See Compressor Cycle sheet for the Tables used for the Saturation Curves in the above plots.  ",null,null,null,null,null,null,null,null,9.5000000000000018,33.139599478943047,719.64770449924686,{"$f":"IF(Y52=1,s_tp1(U52,T52*1000000)/1000,Y52*AC52+(1-Y52)*AB52)","v":1.2696789358407405},285.47880137140351,1,{"$f":"IF(T52*1000000<CO2_PC(),HL_t1(Tsat_P1(T52*1000000))/1000,0)","v":0},{"$f":"IF(T52*1000000<CO2_PC(),HG_T1(Tsat_P1(T52*1000000))/1000,0)","v":0},{"$f":"IF(U52<CO2_TC(),sl_t1(U52)/1000,s_tp1(U52,T52*1000000)/1000)","v":1.2696789358407405},{"$f":"IF(U52<CO2_TC(),sG_T1(U52)/1000,s_tp1(U52,T52*1000000)/1000)","v":1.2696789358407405},{"$f":"IF(U52<CO2_TC(),rhol_t1(U52),rho_tp1(U52,T52*1000000))","v":719.64770449924686},{"$f":"IF(U52<CO2_TC(),rhog_T1(U52),rho_tp1(U52,T52*1000000))","v":719.64770449924686}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,8.4000000000000021,31.106484487113473,702.95515644630132,{"$f":"IF(Y53=1,s_tp1(U53,T53*1000000)/1000,Y53*AC53+(1-Y53)*AB53)","v":1.2747430568224347},285.47880137140351,1,{"$f":"IF(T53*1000000<CO2_PC(),HL_t1(Tsat_P1(T53*1000000))/1000,0)","v":0},{"$f":"IF(T53*1000000<CO2_PC(),HG_T1(Tsat_P1(T53*1000000))/1000,0)","v":0},{"$f":"IF(U53<CO2_TC(),sl_t1(U53)/1000,s_tp1(U53,T53*1000000)/1000)","v":1.2747430568224347},{"$f":"IF(U53<CO2_TC(),sG_T1(U53)/1000,s_tp1(U53,T53*1000000)/1000)","v":1.2747430568224347},{"$f":"IF(U53<CO2_TC(),rhol_t1(U53),rho_tp1(U53,T53*1000000))","v":702.95515644630132},{"$f":"IF(U53<CO2_TC(),rhog_T1(U53),rho_tp1(U53,T53*1000000))","v":702.95515644630132}]
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[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,6.2000000000000028,23.390894301370842,666.29777404709239,{"$f":"IF(Y55=1,s_tp1(U55,T55*1000000)/1000,Y55*AC55+(1-Y55)*AB55)","v":1.2856876324192479},285.47880137140351,0.1316399763761168,{"$f":"IF(T55*1000000<CO2_PC(),HL_t1(Tsat_P1(T55*1000000))/1000,0)","v":268.19009609022828},{"$f":"IF(T55*1000000<CO2_PC(),HG_T1(Tsat_P1(T55*1000000))/1000,0)","v":399.52334118120723},{"$f":"IF(U55<CO2_TC(),sl_t1(U55)/1000,s_tp1(U55,T55*1000000)/1000)","v":1.2273863275620212},{"$f":"IF(U55<CO2_TC(),sG_T1(U55)/1000,s_tp1(U55,T55*1000000)/1000)","v":1.6702708255860133},{"$f":"IF(U55<CO2_TC(),rhol_t1(U55),rho_tp1(U55,T55*1000000))","v":733.26005848578347},{"$f":"IF(U55<CO2_TC(),rhog_T1(U55),rho_tp1(U55,T55*1000000))","v":224.5826317490228}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,5.1000000000000032,15.104034217483775,651.30719061042259,{"$f":"IF(Y56=1,s_tp1(U56,T56*1000000)/1000,Y56*AC56+(1-Y56)*AB56)","v":1.2936226532007948},285.47880137140351,0.25643744012875169,{"$f":"IF(T56*1000000<CO2_PC(),HL_t1(Tsat_P1(T56*1000000))/1000,0)","v":240.30037060294009},{"$f":"IF(T56*1000000<CO2_PC(),HG_T1(Tsat_P1(T56*1000000))/1000,0)","v":416.47757290920356},{"$f":"IF(U56<CO2_TC(),sl_t1(U56)/1000,s_tp1(U56,T56*1000000)/1000)","v":1.1368926295139006},{"$f":"IF(U56<CO2_TC(),sG_T1(U56)/1000,s_tp1(U56,T56*1000000)/1000)","v":1.7480749264834994},{"$f":"IF(U56<CO2_TC(),rhol_t1(U56),rho_tp1(U56,T56*1000000))","v":820.2865955023675},{"$f":"IF(U56<CO2_TC(),rhog_T1(U56),rho_tp1(U56,T56*1000000))","v":161.33677597872884}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,4.0000000000000036,5.3003369391847199,631.38527746240925,{"$f":"IF(Y57=1,s_tp1(U57,T57*1000000)/1000,Y57*AC57+(1-Y57)*AB57)","v":1.305380285935277},285.47880137140351,0.33745555187143744,{"$f":"IF(T57*1000000<CO2_PC(),HL_t1(Tsat_P1(T57*1000000))/1000,0)","v":213.2732753015365},{"$f":"IF(T57*1000000<CO2_PC(),HG_T1(Tsat_P1(T57*1000000))/1000,0)","v":427.24375428590832},{"$f":"IF(U57<CO2_TC(),sl_t1(U57)/1000,s_tp1(U57,T57*1000000)/1000)","v":1.0460701896854796},{"$f":"IF(U57<CO2_TC(),sG_T1(U57)/1000,s_tp1(U57,T57*1000000)/1000)","v":1.814497601271194},{"$f":"IF(U57<CO2_TC(),rhol_t1(U57),rho_tp1(U57,T57*1000000))","v":894.02012026312548},{"$f":"IF(U57<CO2_TC(),rhog_T1(U57),rho_tp1(U57,T57*1000000))","v":115.74031024306727}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Path 5-6-1",{"$f":"$I$11","v":4},{"$f":"$H$11","v":5.3003369391846737},{"$f":"rhog_T1(U58)","v":115.74031024306707},{"$f":"sG_T1(U58)/1000","v":1.8144976012711944}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"$I$11","v":4},{"$f":"$H$11","v":5.3003369391846737},{"$f":"rhol_t1(U59)","v":894.02012026312593},{"$f":"sl_t1(U59)/1000","v":1.0460701896854798}]

{"sheet":"COMPRESSOR CYCLE","index":2,"n_rows":369,"n_cols":31,"rows_kept":369,"cut":false,"hidden":false,"merged":[]}
[null,null,null,null,"COMPRESSOR (Gas Cycle)",null,null,null,null,"SCF Extraction Cycle Energy Requirements (Vapor CO2 feed)"]
[null,null,null,null,null,null,null,null,null,"based the Wagner Equation of State-version 7.0",null,null,null,"Report errors to R.L.Smith. Email: smith@scf.che.tohoku.ac.jp"]
["Based on: R. Span and W. Wagner, A New Equation of State for Carbon Dioxide Covering ",null,null,null,null,null,null,null,null,null,"Version 1.6"]
["the Fluid Regionfrom the Triple-Point Temperature to 1100 K"]
[" at Pressures up to 800 MPa,",null,null,null,null,null,"Point","T [C]","P [MPa]","H [kJ/kg]","X","S [kJ/kg K]","rho [kg/m3]","Comments","HL [kJ/kg]","HG [kJ/kg]","rhoL [kg/m3]","rhoG [kg/m3]","S [kJ/kg K]","S [kJ/kg K]"]
["J. Phys. Chem. Ref. Data 25(6), 1509-1596 (1996).",null,null,null,null,null,2,{"$f":"T_PS1(I6*1000000,L6*1000)","v":75.631557506041233},{"$f":"I8","v":10},{"$f":"H_TP1(H6,I6*1000000)/1000","v":462.45859991146887},{"$f":"IF(AND(J6>O6,J6<P6),(J6-O6)/(P6-O6),1)","v":1},{"$f":"L11","v":1.8144976012711944},{"$f":"rho_tp1(H6,I6*1000000)","v":231.81304863352076},"compressed liquid",{"$f":"IF(H6<CO2_TC(),HL_t1(H6)/1000,H_TP1(H6,I6*1000000)/1000)","v":462.45859991146887},{"$f":"IF(H6<CO2_TC(),HG_T1(H6)/1000,H_TP1(H6,I6*1000000)/1000)","v":462.45859991146887},{"$f":"IF(H6<CO2_TC(),rhol_t1(H6),rho_tp1(H6,I6*1000000))","v":231.81304863352076},{"$f":"IF(H6<CO2_TC(),rhog_T1(H6),rho_tp1(H6,I6*1000000))","v":231.81304863352076},{"$f":"IF(H6<CO2_TC(),sl_t1(H6)/1000,s_tp1(H6,I6*1000000)/1000)","v":1.8144976012713232},{"$f":"IF(H6<CO2_TC(),sG_T1(H6)/1000,s_tp1(H6,I6*1000000)/1000)","v":1.8144976012713232}]
[null,null,null,null,null,null,3,40,10,{"$f":"H_TP1(H7,I7*1000000)/1000","v":313.03932892389435},1,{"$f":"s_tp1(H7,I7*1000000)/1000","v":1.3562366352728115},{"$f":"rho_tp1(H7,I7*1000000)","v":628.6115619691052},"supercritical fluid state-extraction",{"$f":"IF(H7<CO2_TC(),HL_t1(H7)/1000,H_TP1(H7,I7*1000000)/1000)","v":313.03932892389435},{"$f":"IF(H7<CO2_TC(),HG_T1(H7)/1000,H_TP1(H7,I7*1000000)/1000)","v":313.03932892389435},{"$f":"IF(H7<CO2_TC(),rhol_t1(H7),rho_tp1(H7,I7*1000000))","v":628.6115619691052},{"$f":"IF(H7<CO2_TC(),rhog_T1(H7),rho_tp1(H7,I7*1000000))","v":628.6115619691052},{"$f":"IF(H7<CO2_TC(),sl_t1(H7)/1000,s_tp1(H7,I7*1000000)/1000)","v":1.3562366352728115},{"$f":"IF(H7<CO2_TC(),sG_T1(H7)/1000,s_tp1(H7,I7*1000000)/1000)","v":1.3562366352728115}]
[null,null,null,null,null,null,4,{"$f":"H7","v":40},{"$f":"I7","v":10},{"$f":"H_TP1(H8,I8*1000000)/1000","v":313.03932892389435},1,{"$f":"s_tp1(H8,I8*1000000)/1000","v":1.3562366352728115},{"$f":"rho_tp1(H8,I8*1000000)","v":628.6115619691052},"SC fluid state saturated with solute",{"$f":"IF(H8<CO2_TC(),HL_t1(H8)/1000,H_TP1(H8,I8*1000000)/1000)","v":313.03932892389435},{"$f":"IF(H8<CO2_TC(),HG_T1(H8)/1000,H_TP1(H8,I8*1000000)/1000)","v":313.03932892389435},{"$f":"IF(H8<CO2_TC(),rhol_t1(H8),rho_tp1(H8,I8*1000000))","v":628.6115619691052},{"$f":"IF(H8<CO2_TC(),rhog_T1(H8),rho_tp1(H8,I8*1000000))","v":628.6115619691052},{"$f":"IF(H8<CO2_TC(),sl_t1(H8)/1000,s_tp1(H8,I8*1000000)/1000)","v":1.3562366352728115},{"$f":"IF(H8<CO2_TC(),sG_T1(H8)/1000,s_tp1(H8,I8*1000000)/1000)","v":1.3562366352728115}]
[null,null,null,null,null,null,5,{"$f":"T_PH1(I9*1000000,J9*1000)","v":5.3001936865118804},4,{"$f":"J8","v":313.03932892389435},0.46626150117473075,{"$f":"IF(K9<1,K9*T9+(1-K9)*S9,s_tp1(H9,I9*1000000)/1000)","v":1.4043580373603579},{"$f":"IF(K9<1,K9*R9+(1-K9)*Q9,rho_tp1(H9,I9*1000000))","v":531.1384641365903},"System state decided by final enthalpy",{"$f":"IF(H9<CO2_TC(),HL_t1(H9)/1000,H_TP1(H9,I9*1000000)/1000)","v":213.27290653103958},{"$f":"IF(H9<CO2_TC(),HG_T1(H9)/1000,H_TP1(H9,I9*1000000)/1000)","v":427.24386948100755},{"$f":"IF(H9<CO2_TC(),rhol_t1(H9),rho_tp1(H9,I9*1000000))","v":894.02107093148675},{"$f":"IF(H9<CO2_TC(),rhog_T1(H9),rho_tp1(H9,I9*1000000))","v":115.73977195950336},{"$f":"IF(H9<CO2_TC(),sl_t1(H9)/1000,s_tp1(H9,I9*1000000)/1000)","v":1.0460689241725751},{"$f":"IF(H9<CO2_TC(),sG_T1(H9)/1000,s_tp1(H9,I9*1000000)/1000)","v":1.8144984691491277}]
[null,null,null,null,null,null,6,{"$f":"H9","v":5.3001936865118804},{"$f":"I9","v":4},{"$f":"IF(K9=1,J9,P9)","v":427.24386948100755},1,{"$f":"L9","v":1.4043580373603579},{"$f":"rho_tp1(H10,I10*1000000)","v":894.04245075785752},"Saturated vapor",{"$f":"IF(H10<CO2_TC(),HL_t1(H10)/1000,H_TP1(H10,I10*1000000)/1000)","v":213.27290653103958},{"$f":"IF(H10<CO2_TC(),HG_T1(H10)/1000,H_TP1(H10,I10*1000000)/1000)","v":427.24386948100755},{"$f":"IF(H10<CO2_TC(),rhol_t1(H10),rho_tp1(H10,I10*1000000))","v":894.02107093148675},{"$f":"IF(H10<CO2_TC(),rhog_T1(H10),rho_tp1(H10,I10*1000000))","v":115.73977195950336},{"$f":"IF(H10<CO2_TC(),sl_t1(H10)/1000,s_tp1(H10,I10*1000000)/1000)","v":1.0460689241725751},{"$f":"IF(H10<CO2_TC(),sG_T1(H10)/1000,s_tp1(H10,I10*1000000)/1000)","v":1.8144984691491277}]
[null,null,null,null,null,null,1,{"$f":"Tsat_P1(I11*1000000)","v":5.3003369391846737},{"$f":"I10","v":4},{"$f":"HG_T1(H11)/1000","v":427.24375428590838},{"$f":"IF(AND(J11>O11,J11<P11),(J11-O11)/(P11-O11),1)","v":1},{"$f":"sG_T1(H11)/1000","v":1.8144976012711944},{"$f":"rhog_T1(H11)","v":115.74031024306707},"Saturated vapor",{"$f":"IF(H11<CO2_TC(),HL_t1(H11)/1000,H_TP1(H11,I11*1000000)/1000)","v":213.27327530153636},{"$f":"IF(H11<CO2_TC(),HG_T1(H11)/1000,H_TP1(H11,I11*1000000)/1000)","v":427.24375428590838},{"$f":"IF(H11<CO2_TC(),rhol_t1(H11),rho_tp1(H11,I11*1000000))","v":894.02012026312593},{"$f":"IF(H11<CO2_TC(),rhog_T1(H11),rho_tp1(H11,I11*1000000))","v":115.74031024306707},{"$f":"IF(H11<CO2_TC(),sl_t1(H11)/1000,s_tp1(H11,I11*1000000)/1000)","v":1.0460701896854798},{"$f":"IF(H11<CO2_TC(),sG_T1(H11)/1000,s_tp1(H11,I11*1000000)/1000)","v":1.8144976012711944}]
[]
[]
[null,null,null,null,null,null,null,null,null,"Solvent Flow Rate",null,0.3,"kg/s"]
[]
[]
[null,null,null,null,null,null,null,null,null,"Heating and Cooling Requirements"]
[null,null,null,null,null,null,null,null,null,"Q32",{"$f":"(J7-J6)*L14","v":-44.825781296272353},"kW"]
[null,null,null,null,null,null,null,null,null,"Q56",{"$f":"(J10-J9)*L14","v":34.26136216713396},"kW"]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Tables for the Point-to-Point curves in the above plots.  "]
[null,null,null,null,null,null,null,null,null,"Electrical Energy Requirements"]
[null,null,null,null,null,null,null,null,null,"W21",{"$f":"(J6-J11)*L14","v":10.564453687668145},"kW"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"P [MPa]","T [C]","rho [kg/m3]","S [kJ/kg K]","H [kJ/kg]"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Path 1-2",{"$f":"$I$11","v":4},{"$f":"T_PS1(T25*1000000,W25*1000)","v":5.3001936868845281},{"$f":"rho_tp1(U25,T25*1000000)","v":115.7397719602279},{"$f":"$L$11","v":1.8144976012711944}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"T25+($I$6-$I$11)/10","v":4.5999999999999996},15.208570305682326,129.24623693261032,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,5.1999999999999993,24.173689075547113,142.26276414229716,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,5.7999999999999989,32.36241625169508,154.82258543533601,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,6.3999999999999986,39.899580202639186,166.95079148213762,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,6.9999999999999982,46.880395717438134,178.67015822762517,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,7.5999999999999979,53.379909276115129,190.00217155406273,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,8.1999999999999975,59.458910273563859,200.96613791371288,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,8.7999999999999972,65.167363243542056,211.57912318196298,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,9.3999999999999968,70.546691068280637,221.85660435978087,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,9.9999999999999964,75.631557506041219,231.8130486335204,1.8144976012711944]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Path 2-3",{"$f":"$I$6","v":10},{"$f":"$H$6","v":75.631557506041233},231.81304863352076,{"$f":"s_tp1(U36,T36*1000000)/1000","v":1.8144976012713232}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,{"$f":"U36+($H$7-$H$6)/10","v":72.068401755437108},241.47011619928298,{"$f":"s_tp1(U37,T37*1000000)/1000","v":1.793409657298896}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,68.505246004832983,252.71009999993646,{"$f":"s_tp1(U38,T38*1000000)/1000","v":1.7704906812819137}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,64.942090254228859,266.0884278889032,{"$f":"s_tp1(U39,T39*1000000)/1000","v":1.7451904741742503}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,61.378934503624734,282.49461695497706,{"$f":"s_tp1(U40,T40*1000000)/1000","v":1.7166615237472707}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,57.815778753020609,303.46142982633131,{"$f":"s_tp1(U41,T41*1000000)/1000","v":1.683515996958429}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,54.252623002416485,331.87832896197875,{"$f":"s_tp1(U42,T42*1000000)/1000","v":1.6433148960031607}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,50.68946725181236,373.75170783413296,{"$f":"s_tp1(U43,T43*1000000)/1000","v":1.5914863738266849}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,47.126311501208235,441.51700995270807,{"$f":"s_tp1(U44,T44*1000000)/1000","v":1.5201570801946911}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,43.56315575060411,539.76383386665054,{"$f":"s_tp1(U45,T45*1000000)/1000","v":1.4316974037786621}]
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